CN103122108A - Processing assistant for polyvinyl chloride (PVC) and preparation method thereof - Google Patents
Processing assistant for polyvinyl chloride (PVC) and preparation method thereof Download PDFInfo
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- CN103122108A CN103122108A CN2013100146954A CN201310014695A CN103122108A CN 103122108 A CN103122108 A CN 103122108A CN 2013100146954 A CN2013100146954 A CN 2013100146954A CN 201310014695 A CN201310014695 A CN 201310014695A CN 103122108 A CN103122108 A CN 103122108A
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- terephthalate
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- terephthalic acid
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Abstract
The invention relates to a processing assistant for polyvinyl chloride (PVC), which contains polyacrylate (ACR), metal terephthalate, chlorinated paraffin wax and PVC, wherein the metal terephthalate is selected from one or more of calcium terephthalate, magnesium terephthalate, zinc terephthalate, potassium terephthalate, sodium terephthalate, barium terephthalate, lead terephthalate, aluminum terephthalate and iron terephthalate. The invention also relates to a preparation method of the processing assistant. The processing assistant provided by the invention can accelerate the plastication of the PVC, reduce the melt viscosity and lower the energy consumption and production cost; the invention can enhance the flame retardancy of the PVC product on the premise of improving the working properties of the PVC; the invention enhances surface smoothness and aging resistance of the product, and ensures the long-term stability of the product; and the price is lower than ACR, thereby lowering the raw material cost of the processing plant.
Description
Technical field
The present invention relates to a kind of novel polyvinyl-chloride use processing aid and preparation method thereof.
Background technology
Polyvinyl chloride (PVC) is a kind of important commodity polymer material, and since the thirties in 20th century, its field such as plastic window frame in film, sheet material, tubing and exploitation in recent years is widely used.Owing to having defective in the PVC molecular structure, its flow temperature and decomposition temperature approach, and contain two keys, branch point and initiator residue etc. in its molecular structure, add man-hour under high temperature and shear conditions, easily slough the HCl on molecule and cause polymer degradation, color burn, mechanical property reduces, until lose use value.The method that overcomes these defectives has two kinds, and the one, add thermo-stabilizer, improve the thermal stability of PVC; The 2nd, add processing aid, reduce its plasticization temperature.
The processing aid of low molecular mass and the consistency of PVC are poor, auxiliary agent can move, and causes product properties, permanent stability and dimensional stability to reduce, the lost of life, this will inevitably affect the steady progression of PVC material, and environment and recovery are brought heavy pressure.Generally acknowledge that at present best processing aid is mainly ACR, its good processability, weather resistance is excellent, and shock strength is high.But its complex manufacturing, cost is high, and the ACR performance that different copolymerization compositions can cause obtaining differs greatly, and also therefore can cause the control disadvantageous effect quality of item to its consumption and processing temperature.
Summary of the invention
The object of the invention is to prepare a kind of low cost, stable performance, can improve polyvinyl chloride processing aid of goods processing characteristics and preparation method thereof.
The technical solution adopted in the present invention is: a kind of polyvinyl-chloride use processing aid, contain polyacrylic ester (ACR), terephthaldehyde's acid metal salt, clorafin, polyvinyl chloride.
As preferably, described terephthaldehyde's acid metal salt is selected from one or more in terephthalic acid calcium, terephthalic acid magnesium, terephthalic acid zinc, potassium terephthalate, para-phthalic sodium, terephthalic acid barium, terephthaldehyde's lead plumbate, terephthalic acid aluminium, terephthalic acid iron.
As preferably, the mass ratio of polyacrylic ester (ACR), terephthaldehyde's acid metal salt, clorafin, polyvinyl chloride is 25-50: 30-55: 5-10: 5-10.
As preferably, vector resin, terephthaldehyde's acid metal salt, silane coupling agent and and the mass ratio of lubricant be 25-40: 50-70: 7-8: 7-8
The prilling process of aforementioned processing aid, its processing step is: by proportioning terephthaldehyde's acid metal salt and polyacrylic ester are turned at 500-1000 in stirring tank/stir 4min under min, jump to again at 4000-5000 turn/min under high-speed stirring 5min, change 1500-2000 to turn/min under middling speed slowly add clorafin, stir 5min, add again vector resin, stir hot melt mix and blend 10min under 150 ℃, the material that to process at last extrudes under 90-100 ℃, fervent, air-cooled, namely get gained processing aid product of the present invention.
Processing aid provided by the invention can promote the plasticizing of polyvinyl chloride (PVC), reduces its melt viscosity, reduces energy consumption and production costs; When improving the PVC processing characteristics, can improve the flame retardant properties of PVC goods; Improve surface smoothness and the ageing-resistant performance of goods, guarantee the performance steady in a long-term of goods; Price has reduced the material cost of source mill lower than ACR.
Embodiment
Embodiment 1: 55 parts of terephthalic acid calcium and 25 parts of polyacrylic ester are turned 1000 in stirring tank/stir 4min under min, jump to again 5000 turn/min under high-speed stirring 5min, change 2000 turn/min under middling speed slowly add 10 parts of clorafins, stir 5min, add again 10 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 100 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 2: 50 parts of terephthalic acid magnesium and 30 parts of polyacrylic ester are turned 500 in stirring tank/stir 4min under min, jump to again 4000 turn/min under high-speed stirring 5min, change 1500 turn/min under middling speed slowly add 10 parts of clorafins, stir 5min, add again 10 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 90 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 3: with turn 800 in 40 parts of terephthalic acid zinc and 40 parts of polyacrylic ester stirring tanks/stir 4min under min, jump to again 4500 turn/min under high-speed stirring 5min, change 1200 turn/min under middling speed slowly add 5 parts of clorafins, stir 4min, add again 5 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 100 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 4: 30 parts of potassium terephthalates and 55 parts of polyacrylic ester are turned 700 in stirring tank/stir 4min under min, jump to again 5000 turn/min under high-speed stirring 5min, change 1200 turn/min under middling speed slowly add 7 parts of clorafins, stir 5min, add again 8 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 90 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 5: with 25 parts of terephthalic acid calcium, 20 parts of para-phthalic sodiums and 40 parts of polyacrylic ester turn 800 in stirring tank/stir 4min under min, jump to again 4000 turn/min under high-speed stirring 5min, change 1800 turn/min under middling speed slowly add 8 parts of clorafins, stir 5min, add again 7 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 95 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 6: with 10 parts of terephthalic acid barium, 10 parts of terephthalic acid zinc, 16 parts of terephthalic acid magnesium and 50 parts of polyacrylic ester turn 800 in stirring tank/stir 4min under min, jump to again 5000 turn/min under high-speed stirring 5min, change 1300 turn/min under middling speed slowly add 7 parts of clorafins, stir 5min, then add 7 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 90 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 7: 35 parts of terephthaldehyde's lead plumbates and 45 parts of polyacrylic ester are turned 700 in stirring tank/stir 4min under min, jump to again 4000 turn/min under high-speed stirring 5min, change 1400 turn/min under middling speed slowly add 10 parts of clorafins, stir 5min, add again 10 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 100 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 8: 20 parts of terephthalic acid aluminium, 29 parts of terephthaldehyde's lead plumbates and 35 parts of polyacrylic ester are turned 1000 in stirring tank/stir 4min under min, jump to again 5000 turn/min under high-speed stirring 5min, change 2000 turn/min under middling speed slowly add 8 parts of clorafins, stir 5min, add again 8 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 100 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 9: 45 parts of terephthalic acid iron and 40 parts of polyacrylic ester are turned 500 in stirring tank/stir 4min under min, jump to again 4000 turn/min under high-speed stirring 4min, change 1500 turn/min under middling speed slowly add 8 parts of clorafins, stir 3min, add again 7 parts of PVC, stir hot melt mix and blend 10min under 150 ℃.The material that to process at last extrudes under 100 ℃, fervent, air-cooled, namely get gained master batch product of the present invention.
Embodiment 10: with the processing aid (embodiment 1-9) of gained of the present invention,, 5 parts of traditional polyacrylic ester (ACR) and polyvinyl chloride (100 parts) blend, compound adds torque rheometer to carry out the measurement of fusion time and moment of torsion, separately make plastics film, carrying out mechanical property detects, the national standard of each measured performance parameter method institute foundation is specific as follows: tensile strength is pressed GB/T1701-2001 and is measured, elongation at break is pressed GB/T 1701-2001 and is measured, and oxygen index is pressed GB/T 2046[1] .2-2009 mensuration.Detect data such as following table:
From experimental data as can be known, the processing aid of gained of the present invention can promote the plasticizing of PVC, reduces its melt viscosity, reduces energy consumption and production costs; And can improve the PVC processing characteristics; Also can improve simultaneously the flame retardant properties of PVC goods; And preparation technology of the present invention is simple, and price is starkly lower than ACR, has reduced the material cost of source mill.
Take above-mentioned foundation desirable embodiment of the present invention as enlightenment, by above-mentioned description, the relevant staff can in the scope that does not depart from this invention technological thought, carry out various change and modification fully.The technical scope of this invention is not limited to the content on specification sheets, must determine its technical scope according to the claim scope.
Claims (4)
1. a polyvinyl-chloride use processing aid, is characterized in that: contain polyacrylic ester (ACR), terephthaldehyde's acid metal salt, clorafin, polyvinyl chloride.
2. polyvinyl-chloride use processing aid as claimed in claim 1, it is characterized in that: described terephthaldehyde's acid metal salt is selected from one or more in terephthalic acid calcium, terephthalic acid magnesium, terephthalic acid zinc, potassium terephthalate, para-phthalic sodium, terephthalic acid barium, terephthaldehyde's lead plumbate, terephthalic acid aluminium, terephthalic acid iron.
3. polyvinyl-chloride use processing aid as claimed in claim 1, it is characterized in that: the mass ratio of polyacrylic ester (ACR), terephthaldehyde's acid metal salt, clorafin, polyvinyl chloride is 25-50: 30-55: 5-10: 5-10.
4. as the prilling process of polyvinyl-chloride use processing aid as described in the claims 1 to 3 any one, it is characterized in that its processing step is: by proportioning terephthaldehyde's acid metal salt and polyacrylic ester are turned at 500-1000 in stirring tank/stir 4min under min, jump to again at 4000-5000 turn/min under high-speed stirring 5min, change 1500-2000 to turn/min under middling speed slowly add clorafin, stir 5min, add again vector resin, stir hot melt mix and blend 10min under 150 ℃, the material that to process is at last extruded under 90-100 ℃, earnestly, air-cooled, namely get gained processing aid product of the present invention.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104610041A (en) * | 2015-01-26 | 2015-05-13 | 江苏爱特恩东台新材料科技有限公司 | Preparation method for protective material for polyester |
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JP2001139744A (en) * | 1999-11-15 | 2001-05-22 | Shin Etsu Chem Co Ltd | Vinyl chloride-based resin composition |
CN1760256A (en) * | 2004-10-15 | 2006-04-19 | 山东隆发钢板有限公司 | Faceplate of rigid polyvinyl chloride, and producing method |
CN1927934A (en) * | 2006-09-19 | 2007-03-14 | 上海电缆研究所 | Semi-horniness flame-proof PVC sheath material for high-voltage cable |
CN101362846A (en) * | 2007-08-09 | 2009-02-11 | 新疆天业(集团)有限公司 | Nano material modified PVC water transfer hosetube |
EP2145914A2 (en) * | 2008-07-19 | 2010-01-20 | Lanxess Deutschland GmbH | Softener preparations |
CN102153806A (en) * | 2011-04-20 | 2011-08-17 | 江苏爱特恩高分子材料有限公司 | Plastic filling master batch and preparation method thereof |
CN102174235A (en) * | 2011-03-21 | 2011-09-07 | 宜兴市光辉包装材料有限公司 | Calcium/zinc thermal stabilizer polyvinyl chloride transparent hard film and preparation method thereof |
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- 2013-01-16 CN CN2013100146954A patent/CN103122108A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2001139744A (en) * | 1999-11-15 | 2001-05-22 | Shin Etsu Chem Co Ltd | Vinyl chloride-based resin composition |
CN1760256A (en) * | 2004-10-15 | 2006-04-19 | 山东隆发钢板有限公司 | Faceplate of rigid polyvinyl chloride, and producing method |
CN1927934A (en) * | 2006-09-19 | 2007-03-14 | 上海电缆研究所 | Semi-horniness flame-proof PVC sheath material for high-voltage cable |
CN101362846A (en) * | 2007-08-09 | 2009-02-11 | 新疆天业(集团)有限公司 | Nano material modified PVC water transfer hosetube |
EP2145914A2 (en) * | 2008-07-19 | 2010-01-20 | Lanxess Deutschland GmbH | Softener preparations |
CN102174235A (en) * | 2011-03-21 | 2011-09-07 | 宜兴市光辉包装材料有限公司 | Calcium/zinc thermal stabilizer polyvinyl chloride transparent hard film and preparation method thereof |
CN102153806A (en) * | 2011-04-20 | 2011-08-17 | 江苏爱特恩高分子材料有限公司 | Plastic filling master batch and preparation method thereof |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104610041A (en) * | 2015-01-26 | 2015-05-13 | 江苏爱特恩东台新材料科技有限公司 | Preparation method for protective material for polyester |
CN104610041B (en) * | 2015-01-26 | 2016-06-29 | 江苏爱特恩东台新材料科技有限公司 | A kind of preparation method of polyester protective material |
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Application publication date: 20130529 |